JP3200811B2 - Manufacturing method and apparatus for civil engineering materials using coal ash as a main raw material - Google Patents
Manufacturing method and apparatus for civil engineering materials using coal ash as a main raw materialInfo
- Publication number
- JP3200811B2 JP3200811B2 JP30644897A JP30644897A JP3200811B2 JP 3200811 B2 JP3200811 B2 JP 3200811B2 JP 30644897 A JP30644897 A JP 30644897A JP 30644897 A JP30644897 A JP 30644897A JP 3200811 B2 JP3200811 B2 JP 3200811B2
- Authority
- JP
- Japan
- Prior art keywords
- gypsum
- coal ash
- lime
- coal
- amount
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
- C04B28/18—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing mixtures of the silica-lime type
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00034—Physico-chemical characteristics of the mixtures
- C04B2111/00198—Characterisation or quantities of the compositions or their ingredients expressed as mathematical formulae or equations
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Devices For Post-Treatments, Processing, Supply, Discharge, And Other Processes (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、微粉炭焚ボイラ等
から排出される石炭灰に石灰(消石灰又は/及び生石
灰)及び石膏を適正量加え、水で混練した後、成形、養
生して固化・安定化させることにより、路盤材、埋立資
材等の土木資材を製造する方法及び装置に関するもので
ある。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to coal ash discharged from pulverized coal-fired boilers and the like, to which appropriate amounts of lime (slaked lime and / or quick lime) and gypsum are added, kneaded with water, molded, cured and solidified. The present invention relates to a method and an apparatus for manufacturing civil engineering materials such as roadbed materials and landfill materials by stabilizing the materials.
【0002】[0002]
【従来の技術】微粉炭焚ボイラ等から排出される石炭灰
(フライアッシュ)は、セメント原料等として約50%
が再利用され、残りは廃棄物として埋立処分されてい
る。一方、石炭は燃料としての需要が高まっており、石
炭火力発電所等の新設・増設により灰量が増大してい
る。国土の高度利用が進んでいる我国では、今後、灰捨
て場の確保がますます困難になり、また、灰処理費用が
高騰してくると考えられ、大量発生が予想される石炭灰
の再資源化・有効利用技術の開発が要望されている。2. Description of the Related Art Coal ash (fly ash) discharged from a pulverized coal-fired boiler or the like is about 50% as a raw material for cement or the like.
Has been recycled and the rest has been landfilled as waste. On the other hand, demand for coal as fuel is increasing, and the amount of ash is increasing due to the construction and expansion of coal-fired power plants. In Japan, where the advanced utilization of the land is progressing, it will become increasingly difficult to secure ash dumps in the future, and ash disposal costs are expected to rise. There is a demand for the development of technology for effective and effective utilization.
【0003】従来、石炭灰を主原料として固化体(硬化
体)を製造する方法として、例えば、特公昭64−14
17号公報に記載されているように、石炭灰60〜85
重量%、消石灰10〜25重量%、2水石膏8〜25重
量%からなる混合粉体に、水を添加して混練した後、こ
の混練物を型枠又は成形容器を用いて成形し、ついで、
この成形体を80〜100℃の常圧水蒸気で養生処理方
法が知られている。Conventionally, as a method for producing a solidified body (hardened body) using coal ash as a main raw material, for example, Japanese Patent Publication No. Sho 64-14
As described in Japanese Patent Publication No. 17, coal ash 60 to 85
Water and 10 to 25% by weight of slaked lime, and 8 to 25% by weight of gypsum are added to water and kneaded. The kneaded product is molded using a mold or a molding container. ,
There is known a curing treatment method for the molded body with normal pressure steam at 80 to 100 ° C.
【0004】また、特開平8−59311号公報には、
石炭焚流動層ボイラへ供給する脱硫剤としての石灰石量
を、燃焼灰中の生石灰量が10〜30wt%となるよう
に、石炭中の灰分量及び/又は石炭中の硫黄分量に応じ
て調整し、成分調整された燃焼灰を水と混練し、混練物
を成形した後、養生する流動層燃焼灰を原料とする固化
体の製造方法が記載されている。Japanese Patent Application Laid-Open No. Hei 8-59311 discloses that
The amount of limestone as a desulfurizing agent supplied to the coal-fired fluidized bed boiler is adjusted according to the amount of ash in coal and / or the amount of sulfur in coal so that the amount of quicklime in combustion ash becomes 10 to 30 wt%. A method for producing a solidified body from a fluidized bed combustion ash, which is obtained by kneading a combustion ash having adjusted components with water, forming a kneaded product, and curing the mixture, is described.
【0005】[0005]
【発明が解決しようとする課題】上記の特公昭64−1
417号公報記載の方法は、微粉炭焚ボイラからの石炭
灰に、その性状によらず一定量の消石灰及び石膏を添加
するものであり、この方法では、灰の組成によって添加
材(消石灰及び石膏)が必要以上に消費されコスト高と
なったり、逆に、添加材が少なく強度不足の固化体とな
ったりする。また、上記の特開平8−59311号公報
記載の方法は、石炭焚流動層ボイラからの石炭灰から粒
状固化体を製造し路盤材とするものであり、この方法で
は、路盤材の材料である灰の組成は成り行き任せで、固
化体の強度をコントロールすることはできず、灰組成に
よっては不良品が大量にできてしまうことになる。The above-mentioned Japanese Patent Publication No. 64-1
No. 417 discloses a method of adding a certain amount of slaked lime and gypsum to coal ash from a pulverized coal-fired boiler irrespective of its properties. In this method, additives (slaked lime and gypsum) are added depending on the ash composition. ) Is unnecessarily consumed to increase the cost, and conversely, the solidified material has a small amount of the additive and is insufficient in strength. Further, the method described in the above-mentioned Japanese Patent Application Laid-Open No. 8-59311 is to produce a granular solidified material from coal ash from a coal-fired fluidized bed boiler and use it as a roadbed material. The composition of the ash is up to you, and the strength of the solidified body cannot be controlled. Depending on the ash composition, a large number of defective products will be produced.
【0006】本発明は上記の諸点に鑑みなされたもの
で、本発明の目的は、石炭灰の組成に応じた適正な量の
添加材(石灰及び石膏)を加えることで、最低限の添加
材量で固化体に必要な強度を発現させるようにすること
により、固化体強度をコントロールすることができ、こ
のため、多種の石炭灰に対応することが可能で、かつ、
固化体製造コストを低減することができ、しかも、有害
重金属が水和物に固定されるので安全性を確保すること
ができ、この結果、微粉炭焚ボイラ等からの石炭灰を大
量有効利用することができる石炭灰を主原料とする土木
資材の製造方法及び装置を提供することにある。[0006] The present invention has been made in view of the above points, and an object of the present invention is to minimize the amount of additive by adding an appropriate amount of additive (lime and gypsum) according to the composition of coal ash. By expressing the strength required for the solidified body in an amount, the solidified body strength can be controlled, and therefore, it is possible to cope with various types of coal ash, and
The cost of solidification can be reduced, and safety can be ensured because harmful heavy metals are fixed to hydrates. As a result, a large amount of coal ash from pulverized coal-fired boilers can be effectively used. It is an object of the present invention to provide a method and an apparatus for producing civil engineering materials using coal ash as a main raw material.
【0007】[0007]
【課題を解決するための手段】上記の目的を達成するた
めに、本発明の石炭灰を主原料とする土木資材の製造方
法は、石炭灰にCaO/(SiO2 +Al2 O3 )重量
比が水和反応が十分に進行し、かつSiO 2 及びAl 2
O 3 不足とならない範囲である0.06〜0.2となる
ように石灰(消石灰又は/及び生石灰)を加えて調整混
合物とするとともに、この調整混合物に水和反応が十分
に進行し、かつ未反応の石膏が残存しない範囲である生
石灰に換算した石灰の0.2〜1.0倍、望ましくは
0.25〜0.75倍の重量の石膏を加えて石膏調整混
合物とし、同時にこの石膏調整混合物に混練水を加えて
混練した後、混練物を成形し、ついで、成形物を常温〜
55℃で養生した後、水蒸気養生して、最低限の添加材
量で高強度の固化体を得るように構成されている(図1
〜図7参照)。石灰として消石灰(Ca(OH)2 )を
用いる場合は、Ca(OH)2 を生石灰(CaO)に換
算して、CaO/(SiO2 +Al2 O3 )重量比が
0.06〜0.2の範囲になるように消石灰を添加す
る。この値が0.06未満の場合は、水和反応が十分に
進行せず、固化体の強度が低くなり、良質な土木資材と
はならず、一方、0.2を超える場合は、添加材コスト
が高くなるとともに、SiO2 やAl2 O3 不足とな
り、固化体の強度は低くなり、良質な土木資材とならな
い。なお、石炭灰、石灰、石膏、水の混合順序は問わ
ず、要は、最終的にこれらが混練されれば良い。Means for Solving the Problems To achieve the above object, the present invention relates to a method for producing a civil engineering material using coal ash as a main raw material, wherein the coal ash has a CaO / (SiO 2 + Al 2 O 3 ) weight ratio. Hydrate reaction proceeds sufficiently, and SiO 2 and Al 2
Lime (slaked lime and / or quick lime) is added to adjust the mixture so that the amount becomes 0.06 to 0.2, which is a range that does not cause O 3 deficiency, and the adjusted mixture has a sufficient hydration reaction.
Gypsum having a weight of 0.2 to 1.0 times, preferably 0.25 to 0.75 times the lime converted to quick lime in a range where unreacted gypsum does not remain. In addition, a gypsum adjustment mixture was added, and at the same time, kneading water was added to the gypsum adjustment mixture and kneaded, and then the kneaded product was molded.
After curing at 55 ° C, steam curing to minimize the amount of additive
It is configured to obtain a solid material of high strength in an amount (Fig. 1
To FIG. 7). When using hydrated lime as the lime (Ca (OH) 2), in terms of Ca (OH) 2 in the lime (CaO), CaO / (SiO 2 + Al 2 O 3) weight ratio is 0.06 to 0.2 Slaked lime is added so as to be within the range. If this value is less than 0.06, the hydration reaction does not proceed sufficiently, the strength of the solidified body decreases, and the material does not become a good quality civil engineering material. As the cost increases, SiO 2 and Al 2 O 3 become deficient, the strength of the solidified body decreases, and it does not become a good quality civil engineering material. The order of mixing the coal ash, lime, gypsum, and water is not limited, and it is only necessary that these components are finally kneaded.
【0008】石膏添加量は、石炭灰に添加される生石灰
の重量比で0.2〜1.0倍、望ましくは0.25〜
0.75倍である。なお、消石灰を添加する場合は生石
灰に換算された値を基準とする。石膏添加量が下限未満
の場合は、水和反応が十分に進行せず、固化体の強度が
低くなり、一方、上限を超える場合は、添加材のコスト
が高くなるとともに、未反応の石膏が残存し、固化体の
強度が低くなる。また、混練水としては工業用水又は海
水が用いられ、石膏混合物100重量部に対して20〜
50重量%が加えられる。この場合、30〜60℃の温
水を用いることが好ましい。温水を用いる場合は、固化
体の強度、安定性が向上し、また、冬季、寒冷地におい
ても安定した固化体の品質を確保することができるとい
う利点がある。また、海水を用いる場合は、固化体の強
度がさらに大きくなるという利点がある。[0008] The amount of gypsum added is 0.2 to 1.0 times, preferably 0.25 to 1.0 times the weight ratio of quick lime added to coal ash.
It is 0.75 times. In addition, when adding slaked lime, the value converted into quick lime is used as a reference. When the amount of added gypsum is less than the lower limit, the hydration reaction does not proceed sufficiently, and the strength of the solidified body is reduced.On the other hand, when the amount exceeds the upper limit, the cost of the additive increases and unreacted gypsum is removed. It remains and the strength of the solidified body decreases. Further, industrial water or seawater is used as the kneading water, and 20 to 100 parts by weight of the gypsum mixture is used.
50% by weight are added. In this case, it is preferable to use warm water of 30 to 60 ° C. When hot water is used, the strength and stability of the solidified body are improved, and there is an advantage that stable quality of the solidified body can be ensured even in winter and cold regions. When seawater is used, there is an advantage that the strength of the solidified body is further increased.
【0009】成形時には、流し込み成形、加圧成形又は
突き固め成形等で所定の形に成形され、その後、常温か
ら55℃の範囲で5〜24時間養生し、さらに60〜9
8℃の飽和水蒸気下で10〜24時間養生する。「常温
〜55℃」における上限の55℃は、強度の低い混練
物、成形物が急激な水和反応による膨張により、クラッ
クが発生しない場合を考慮した値である。常温〜55℃
における養生処理では、水和反応物によって有害重金属
が固定され、埋立判定基準を満足させることができる。
さらに、水蒸気養生処理を行うことにより、水和反応が
より進行し、かつ、遊離石灰がなくなり、有害重金属が
より固定されて、土壌環境基準を満足させることができ
る。養生処理した固化体は、破砕されて粒径40mm以
下、詳しくは、0.05〜40mmの粒度分布を有する粒
状固化体とされて、路盤材、埋立資材等の土木資材とし
て有効利用される。At the time of molding, it is formed into a predetermined shape by cast molding, pressure molding or tamping molding, and then cured at room temperature to 55 ° C. for 5 to 24 hours.
Cure under saturated steam at 8 ° C for 10 to 24 hours. The upper limit of 55 ° C. in “normal temperature to 55 ° C.” is a value in consideration of a case where a kneaded product or molded product having low strength does not crack due to expansion due to a rapid hydration reaction. Room temperature to 55 ° C
In the curing treatment in the above, the harmful heavy metal is fixed by the hydration reaction product, and the landfill determination standard can be satisfied.
Furthermore, by performing the steam curing treatment, the hydration reaction proceeds further, free lime is eliminated, and harmful heavy metals are more fixed, so that the soil environmental standards can be satisfied. The cured solidified product is crushed to be a granular solidified product having a particle size distribution of 40 mm or less, specifically 0.05 to 40 mm, and is effectively used as a civil engineering material such as a roadbed material and a landfill material.
【0010】石炭灰に添加する石灰及び石膏の量を、ボ
イラで燃焼させる石炭の灰分組成、例えば、灰分のCa
O/(SiO2 +Al2 O3 )重量比に基づいて制御す
るように構成したり、又は、石炭灰を電気集塵機のホッ
パや中継ホッパ等のホッパ下又は気流搬送過程で採取
し、石炭灰の蛍光X線によるCaO/(SiO2 +Al
2 O3 )重量比の測定を行い、該測定値に基づいて石灰
及び石膏の添加量を制御するように構成する。また、石
膏として、排煙脱硫装置から得られた石膏を用い、この
石膏を石炭灰の一部又は石灰の一部とともに粉砕して、
ブレーン比表面積を2500cm2 /g以上としたものを
石炭灰に添加することが好ましい(図4〜図7参照)。
なお、系外から石膏を搬入して用いることも、勿論可能
である。また、石灰として、石灰石及び貝殻の少なくと
もいずれかを焼成して生石灰とし、この生石灰を粉砕し
てブレーン比表面積を2500cm2 /g 以上としたもの
を用いる場合もある(図6、図7参照)。ここで、ブレ
ーン比表面積とは、JIS R 5201(セメントの
物理試験方法)に示されているブレーン空気透過装置を
用いて測定された値で、粒子の細かさを示す指標を言
う。石膏や石灰のブレーン比表面積が2500cm2 /g
未満の場合は、水和反応性がよくなく、得られる処理物
(固化体)の圧縮強度が十分でなく、重金属の溶出の可
能性が生じる。ブレーン比表面積が大きくなるに従って
水和反応性がよくなって、固化体の圧縮強度が高まるも
のの、経済的に不利になる。したがって、ブレーン比表
面積の上限は限定されるものではないが、実用上、1
0,000cm2 /g を上限とすることが好ましい。The amount of lime and gypsum added to the coal ash is determined by the ash composition of the coal burned in the boiler, for example, the ash content Ca
O / (SiO 2 + Al 2 O 3 ) weight ratio may be controlled, or coal ash may be collected under a hopper such as a hopper of an electric dust collector or a relay hopper or in an air flow conveying process, and the coal ash may be collected. CaO / (SiO 2 + Al) by fluorescent X-ray
2 O 3) performs a measurement of the weight ratio, configured to control the amount of lime and gypsum based on measured values. In addition, as gypsum, using gypsum obtained from a flue gas desulfurization device, crushing this gypsum together with part of coal ash or part of lime,
It is preferable to add a material having a brane specific surface area of 2500 cm 2 / g or more to coal ash (see FIGS. 4 to 7).
Of course, it is also possible to carry gypsum from outside the system and use it. In some cases, lime is used by calcining at least one of limestone and shell to form quicklime, and pulverizing the quicklime to have a Blaine specific surface area of 2500 cm 2 / g or more (see FIGS. 6 and 7). . Here, the Blaine specific surface area is a value measured using a Blaine air permeation apparatus described in JIS R 5201 (physical test method for cement) and is an index indicating the fineness of particles. Plain or lime with a specific surface area of 2,500 cm 2 / g
If it is less than 1, the hydration reactivity is not good, and the compressive strength of the obtained treated product (solidified product) is not sufficient, and the possibility of elution of heavy metals occurs. As the Blaine specific surface area increases, the hydration reactivity increases, and the compressive strength of the solidified body increases, but it is economically disadvantageous. Therefore, the upper limit of the brane specific surface area is not limited, but is practically 1
It is preferable that the upper limit is set to 0.000 cm 2 / g.
【0011】本発明の石炭灰を主原料とする土木資材の
製造装置は、石炭焚ボイラからの排ガスを導入して排ガ
ス中に含まれる石炭灰を捕集する集塵機と、捕集された
石炭灰を導入し石灰、石膏及び水とともに混練する混練
機と、混練機からの混練物を成形する成形機と、成形機
からの成形物を養生する養生装置とを備えた石炭灰処理
装置において、ホッパ又は気流搬送過程で採取された石
炭灰のCaO/(SiO2 +Al2 O3 )重量比の測定
を行う品質管理装置を設け、この品質管理装置により石
炭灰に添加する石灰及び石膏の量を制御することができ
るように、この品質管理装置と石灰供給機及び石膏供給
機とが連動接続されて、石炭灰−石灰−石膏系混合物か
らなる固化体を得るようにしたことを特徴としている
(図1、図4、図6参照)。[0011] The present invention relates to an apparatus for producing civil engineering materials using coal ash as a main material, comprising: a dust collector for introducing exhaust gas from a coal-fired boiler to collect coal ash contained in the exhaust gas; A kneader for introducing kneading and kneading with lime, gypsum and water, a molding machine for molding the kneaded material from the kneading machine, and a curing device for curing the molded product from the molding machine, a hopper, or coal ash collected by the pneumatic conveying process CaO / (SiO 2 + Al 2 O 3) ratio by weight of the measurement
The quality control device that performs provided, so as to be able to control the amount of lime and gypsum to be added to the coal ash by the quality control apparatus, and the quality control device and lime feeder and gypsum feeder is interlocked connected And a solidified material comprising a coal ash-lime-gypsum-based mixture is obtained (see FIGS. 1, 4 and 6).
【0012】また、本発明の土木資材製造装置は、石炭
焚ボイラからの排ガスを導入して排ガス中に含まれる石
炭灰を捕集する集塵機と、捕集された石炭灰を導入し石
灰、石膏及び水とともに混練する混練機と、混練機から
の混練物を成形する成形機と、成形機からの成形物を養
生する養生装置とを備えた石炭灰処理装置において、前
記石炭焚ボイラで燃焼させる石炭の炭種の灰分組成から
CaO/(SiO2 +Al2 O3 )重量比を計算し石炭
灰に添加する石灰及び石膏の量を決定する品質管理装置
を設け、この品質管理装置により石炭灰に添加する石灰
及び石膏の量を制御することができるように、この品質
管理装置と石灰供給機及び石膏供給機とが連動接続され
て、石炭灰−石灰−石膏系混合物からなる固化体を得る
ようにしたことを特徴としている(図3、図5、図7参
照)。これらの土木資材製造装置において、養生装置の
後流に、養生物を破砕するための破砕機を設けて、石炭
灰−石灰−石膏混合物からなる粒状の固化体を得るよう
に構成することが好ましい。[0012] Further, the present invention provides an apparatus for producing civil engineering materials, comprising: a dust collector for introducing exhaust gas from a coal-fired boiler to collect coal ash contained in the exhaust gas; and a lime and gypsum for introducing the collected coal ash to collect ash. And a kneading machine for kneading with water, a molding machine for molding the kneaded material from the kneading machine, and a curing device for curing the molded product from the molding machine. A quality control device for calculating the CaO / (SiO 2 + Al 2 O 3 ) weight ratio from the ash composition of the coal type of coal and determining the amount of lime and gypsum added to the coal ash is provided. In order to control the amount of lime and gypsum to be added, the quality control device and the lime feeder and the gypsum feeder are connected in conjunction with each other so as to obtain a solidified body composed of a coal ash-lime-gypsum-based mixture. What you did Is set to characters (3, 5, see FIG. 7). In these civil engineering material production devices, it is preferable to provide a crusher for crushing the cured organisms downstream of the curing device, so as to obtain a particulate solidified body composed of a coal ash-lime-gypsum mixture. .
【0013】微粉炭焚ボイラ灰のみでは、水を加えても
高強度の固化体とならず、大半は廃棄されており、性状
が安定していない等の理由で大量有効利用が殆ど行われ
ていない。しかし、石炭灰には可溶性のSiO2 、Al
2 O3 が多く含まれているために、石灰や石膏を添加す
るとポゾラン反応が促進され、不溶性のC−S−H(ケ
イ酸カルシウム水和物)ゲルやエトリンガイトを生成し
高強度の固化体となる。また、灰中の重金属は、エトリ
ンガイトやC−S−H中に取り込まれ、化学的に安定化
される。このように、石炭灰を固化・安定化し路盤材、
埋立資材等の土木資材とすることで大量有効利用を図る
ものである。また、それぞれの灰組成に応じた適正な量
の石灰及び石膏を加えることで、最小限の石灰添加量及
び石膏添加量で必要な強度を発現させる。目標の一軸圧
縮強度を100kg/cm2 とすると、石灰添加量は消石灰
で2〜9%、石膏添加量は1〜6%である。このよう
に、石灰及び石膏の添加量を制御することにより固化体
強度をコントロールすることができ、多種の石炭灰に容
易に対応することができる。[0013] The pulverized coal-fired boiler ash alone does not become a high-strength solidified substance even when water is added, and most of the ash is discarded, and its effective use in large quantities is mostly performed because its properties are not stable. Absent. However, coal ash has soluble SiO 2 , Al
The addition of lime or gypsum promotes the pozzolanic reaction because it contains a large amount of 2 O 3 , and forms an insoluble CSH (calcium silicate hydrate) gel or ettringite to form a high-strength solidified product. Becomes In addition, heavy metals in the ash are taken into ettringite and C—S—H and are chemically stabilized. In this way, coal ash is solidified and stabilized,
It is intended to be used effectively in large quantities by using civil engineering materials such as landfill materials. Further, by adding appropriate amounts of lime and gypsum according to each ash composition, the required strength is developed with the minimum amount of lime and gypsum added. Assuming that the target uniaxial compressive strength is 100 kg / cm 2 , the added amount of lime is 2 to 9% for slaked lime and the added amount of gypsum is 1 to 6%. As described above, by controlling the amounts of lime and gypsum added, the strength of the solidified body can be controlled, and it is possible to easily cope with various types of coal ash.
【0014】石灰及び石膏を適正量添加するためには、
燃焼させる石炭の灰分組成に基づき石灰及び石膏の添加
量を決定するか、又は、石炭灰をホッパ下もしくは気流
搬送管より採取し、手分析又はオンラインで蛍光X線に
よるCa、Al、Siの分析を行い、分析値に応じて石
灰添加量及び石膏添加量を決定する。石灰系の添加材と
してはセメントも考えられるが、セメント添加では同一
強度を発現させるために添加材量(セメント量)が消石
灰添加の場合の2〜2.5倍になり、セメントは消石灰
の約1/2のコストであるので添加材コストはほぼ等し
いが、灰重量ベースで考えると、消石灰又は生石灰を使
用することで固化体製造コストの低減を図ることができ
る。In order to add lime and gypsum in appropriate amounts,
Determine the amount of lime and gypsum to be added based on the ash composition of the coal to be burned, or collect the coal ash under a hopper or from a pneumatic conveying pipe, and analyze Ca, Al, Si by manual analysis or online X-ray fluorescence. The amount of lime and the amount of gypsum added are determined according to the analysis value . Cement is also considered as a lime-based additive, but the amount of additive (cement) is 2 to 2.5 times that of slaked lime in order to achieve the same strength with cement addition. Since the cost of the additive material is 1/2, the cost of the additive material is almost the same. However, considering the ash weight basis, the use of slaked lime or quick lime can reduce the production cost of the solidified body.
【0015】また、石灰源として、本発明の土木資材製
造装置に石灰石や貝殻を焼成する焼成炉(流動層炉、シ
ャフト炉等)を併設し、石灰石や貝殻を焼成して生石灰
とすることにより、添加材コストをさらに低減させるこ
とができる。このとき、焼成用燃料として、発電所から
排出される廃油、スラッジ等を燃料の一部とすれば、焼
成コストをさらに低減できるだけでなく、発電所のゼロ
エミッションにも貢献することができる。さらに、前述
のように、エトリンガイト(3CaO・Al2 O3 ・3
CaSO4 ・32H2 O)等の水和生成物が多く生成
し、有害重金属が水和物に固定されるため、環境基準に
より定められた安全基準を確保することができる。Further, as a lime source, a sintering furnace (fluidized bed furnace, shaft furnace, etc.) for sintering limestone and shells is provided in the civil engineering material production apparatus of the present invention, and limestone and shells are sintered to quicklime. In addition, the cost of the additive can be further reduced. At this time, if waste oil, sludge, and the like discharged from the power plant are used as a part of the fuel for firing, not only the firing cost can be further reduced, but also the zero emission of the power plant can be contributed. Further, as described above, ettringite (3CaO.Al 2 O 3 .3)
Since a large amount of hydration products such as CaSO 4 .32H 2 O) are generated and harmful heavy metals are fixed to the hydrate, safety standards defined by environmental standards can be ensured.
【0016】[0016]
【発明の実施の形態】以下、本発明の実施の形態につい
て説明するが、本発明は下記の実施の形態に何ら限定さ
れるものではなく、適宜変更して実施することができる
ものである。図1は本発明の実施の第1形態による石炭
灰を主原料とする土木資材の製造装置を示し、図2は図
1における固化体製造プラント(固化体製造装置)を示
している。図1及び図2において、石炭(例えば、微粉
炭)はボイラ(例えば、微粉炭焚ボイラ)10等の石炭
燃焼装置に供給されて燃焼し、ボイラからの燃焼排ガス
は集塵機、例えば、電気集塵機(EP)12に導入され
て排ガス中に含まれる石炭灰(フライアッシュ)が捕集
される。除塵された排ガスは石灰石スラリー等を吸収液
とする湿式脱硫装置等の脱硫装置14に導入されて排ガ
ス中の硫黄酸化物等が除去される。除去された硫黄酸化
物等は石膏として回収され、石膏ホッパ16に一旦貯留
される。石膏ホッパ16の石膏は、石膏供給機18によ
り固化体製造プラント20に供給される。DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below, but the present invention is not limited to the following embodiments and can be implemented with appropriate modifications. FIG. 1 shows an apparatus for producing civil engineering materials using coal ash as a main raw material according to a first embodiment of the present invention, and FIG. 2 shows a solidified body production plant (solidified body production apparatus) in FIG. 1 and 2, coal (for example, pulverized coal) is supplied to a coal combustion device such as a boiler (for example, pulverized coal-fired boiler) 10 and burns, and combustion exhaust gas from the boiler is collected by a dust collector, for example, an electric dust collector ( The coal ash (fly ash) introduced into the EP 12 and contained in the exhaust gas is collected. The exhaust gas from which dust has been removed is introduced into a desulfurization device 14 such as a wet desulfurization device using a limestone slurry or the like as an absorbing liquid to remove sulfur oxides and the like in the exhaust gas. The removed sulfur oxides and the like are collected as gypsum and temporarily stored in the gypsum hopper 16. The gypsum in the gypsum hopper 16 is supplied to the solidified body manufacturing plant 20 by the gypsum supply machine 18.
【0017】一方、捕集された石炭灰は、一部が品質管
理装置22でサンプリングされて石炭灰ホッパ24に搬
送(例えば、気流搬送)され、一旦貯留される。石炭灰
ホッパ24の石炭灰は、石炭灰供給機26により固化体
製造プラント20に供給される。28は消石灰又は生石
灰を一時貯留するための石灰ホッパで、この石灰ホッパ
28の石灰は、石灰供給機30により固化体製造プラン
ト20に供給される。また、同時に、固化体製造プラン
ト20に混練水が供給される。品質管理装置22は、石
炭灰ホッパ24下の石炭灰供給機(切り出し装置)2
6、石灰ホッパ28下の石灰供給機(切り出し装置)3
0及び石膏ホッパ16下の石膏供給機(切り出し装置)
18をコントロールして、所定量の量を固化体製造プラ
ント20に供給するように構成されている。これらの供
給機18、26、30としては、テーブルフィーダー、
スクリュウフィーダー、ロータリーフィーダー等が用い
られる。On the other hand, part of the collected coal ash is sampled by the quality control device 22, transported to the coal ash hopper 24 (for example, by airflow), and temporarily stored. The coal ash from the coal ash hopper 24 is supplied to the solidified body production plant 20 by a coal ash supply device 26. Reference numeral 28 denotes a lime hopper for temporarily storing slaked lime or quick lime. The lime in the lime hopper 28 is supplied to the solidified body production plant 20 by a lime supply device 30. At the same time, kneading water is supplied to the solidified body manufacturing plant 20. The quality control device 22 includes a coal ash feeder (cutting device) 2 under a coal ash hopper 24.
6. Lime feeder (cutting device) 3 below lime hopper 28
Gypsum feeder (cutting device) below the gypsum hopper 16 and 0
The control unit 18 is configured to supply a predetermined amount to the solidified body manufacturing plant 20 by controlling the same. These feeders 18, 26, 30 include table feeders,
A screw feeder, a rotary feeder, or the like is used.
【0018】固化体製造プラント20は、図2に示すよ
うに、混練機32、成形機34、養生装置36及び破砕
機38からなっている。混練機32としては、逆流式高
速混練機(アイリッヒミキサ)、ヘンシェルミキサ、水
平軸回転混練機、振動式混練機(バイブロミキサ)等の
撹拌造粒が可能な機種以外に、縦軸高速回転混練機(ピ
ンミキサ等)等が適している。成形機34としては、ブ
リケットマシンのような高圧タイプ、押出タイプ、ブロ
ックマシン等のような低圧タイプが適している。また、
養生装置36は、常温又は常温近傍の温度(常温〜55
℃)で養生処理する常温養生処理部、及び60〜98℃
の飽和水蒸気雰囲気で養生処理する水蒸気養生処理部か
らなっている。養生装置36としては、固化体を載せた
ラックが順次出口へと移動しつつ養生処理を行うタイ
プ、コンベアで搬送しながら順次下方へ移行させつつ養
生処理を行うタイプ、縦軸に接合した撹拌翼で撹拌しな
がら順次下方へ移行させつつ養生を行うタイプ等を適用
することができる。また、破砕機38としては、ハンマ
ーミル、インペラーブレーカ、インパクトクラッシャ等
の衝撃式のものが適している。As shown in FIG. 2, the solidified body production plant 20 includes a kneader 32, a molding machine 34, a curing device 36, and a crusher 38. Examples of the kneading machine 32 include, in addition to models capable of stirring and granulating, such as a backflow high-speed kneading machine (Erich mixer), a Henschel mixer, a horizontal axis kneading machine, and a vibrating kneading machine (vibromixer), a vertical axis high-speed kneading machine. A kneader (such as a pin mixer) is suitable. As the molding machine 34, a high-pressure type such as a briquette machine, an extrusion type, a low-pressure type such as a block machine is suitable. Also,
The curing device 36 is provided at a normal temperature or a temperature near normal temperature (normal temperature to 55
℃), and a room temperature curing treatment section for curing at 60-98 ° C
A steam curing section for curing in a saturated steam atmosphere. As the curing device 36, a type in which a rack on which the solidified body is placed is sequentially moved to an outlet to perform a curing process, a type in which a curing process is performed while sequentially moving downward while being transported by a conveyor, and a stirring blade joined to the vertical axis A type in which curing is performed while sequentially moving downward with stirring can be applied. Further, as the crusher 38, an impact type such as a hammer mill, an impeller breaker, and an impact crusher is suitable.
【0019】品質管理装置22は、サンプリングされた
石炭灰のCaO/(SiO2 +Al2 O3 )重量比の測
定を行い、CaO/(SiO2 +Al2 O3 )重量比が
0.06〜0.2となるように石灰添加量を制御し、か
つ、石膏添加量が生石灰に換算した石灰の0.2〜1.
0倍になるように石膏添加量を制御するように構成され
ている。The quality control device 22 measures the CaO / (SiO 2 + Al 2 O 3 ) weight ratio of the sampled coal ash.
The amount of lime added was controlled so that the CaO / (SiO 2 + Al 2 O 3 ) weight ratio was 0.06 to 0.2, and the amount of gypsum added was 0.2% of lime converted to quick lime. ~ 1.
The gypsum addition amount is controlled to be 0 times.
【0020】上記のように構成された土木資材の製造装
置において、石炭灰を電気集塵機のホッパ、中継ホッパ
等のホッパ下又は気流搬送過程で採取し、石炭灰のCa
O/(SiO2 +Al2 O3 )重量比を測定し、測定値
に基づいて、CaO/(SiO2 +Al2 O3 )重量比
が0.06〜0.2の範囲の所定値となるように、か
つ、石膏量が生石灰に換算した石灰の0.2〜1.0倍
の範囲の所定値となるように、供給機26、30、18
を制御して、混練機32へ供給する石炭灰量、石灰量及
び石膏量を調節する。同時に、混練機32に石炭灰・石
灰・石膏混合物100重量部に対して20〜50重量%
の水を加えて混練する。ついで、混練物を成形機34で
所定の形状(例えば、アーモンド状、円柱状、ブロック
状等)に成形した後、成形物を養生装置36で常温〜5
5℃の範囲で5〜24時間養生し、さらに、60〜98
℃の飽和水蒸気下で10〜24時間養生する。そして、
養生物を破砕機38で不定形の40mm以下(0.05〜
40mm)の粒状体とする。破砕処理により、破砕処理物
(粒状体)の修正CBRが80%以上となり、路盤材、
埋立資材等の土木資材として有効利用することができ
る。ここで、修正CBRとは、路盤材などの土木資材と
して用いられる粒状材料の強さを示す指標で、大きい
程、強さがすぐれており、JIS A 1211(路床
土支持力比(CBR)試験方法)に示す方法に準じて、
3層に分けて各層92回突固めたときの最大乾燥密度に
対する所要の締固め度に相当する水浸CBRを言う。In the civil engineering material manufacturing apparatus constructed as described above, coal ash is collected under a hopper such as a hopper of an electric dust collector, a relay hopper, or in an air flow conveying process, and the coal ash Ca is collected.
The O / (SiO 2 + Al 2 O 3 ) weight ratio is measured, and based on the measured value, the CaO / (SiO 2 + Al 2 O 3 ) weight ratio becomes a predetermined value in the range of 0.06 to 0.2. So that the amount of gypsum becomes a predetermined value in the range of 0.2 to 1.0 times the lime converted to quick lime.
Is controlled to adjust the amount of coal ash, the amount of lime and the amount of gypsum supplied to the kneading machine 32. At the same time, the kneader 32 is 20 to 50% by weight based on 100 parts by weight of the coal ash / lime / gypsum mixture.
Add water and knead. Next, after the kneaded material is formed into a predetermined shape (for example, almond shape, column shape, block shape, etc.) by the molding machine 34, the formed material is cured at room temperature to 5 ° C. by the curing device 36.
Cured at 5 ° C for 5 to 24 hours, and then 60-98
Cured under saturated steam at 10 ° C for 10 to 24 hours. And
The cultivated organism is crushed by the crusher 38 to an irregular 40 mm or less (0.05 to
40 mm). By the crushing process, the modified CBR of the crushed product (granular material) becomes 80% or more, and the roadbed material,
It can be effectively used as civil engineering material such as landfill material. Here, the modified CBR is an index indicating the strength of a granular material used as a civil engineering material such as a roadbed material. The larger the larger, the better the strength is, and the JIS A 1211 (subgrade soil bearing capacity ratio (CBR)) Test method)
It refers to a water immersion CBR corresponding to a required degree of compaction with respect to the maximum dry density when each layer is compacted 92 times in three layers.
【0021】図3は本発明の実施の第2形態による土木
資材製造装置を示している。本実施形態は、実施の第1
形態における品質管理装置22の代りに、ボイラで燃焼
させる石炭の灰分のCaO/(SiO2 +Al2 O3 )
重量比から石炭灰に添加する石灰添加量及び石膏添加量
を決定し、添加量を制御する品質管理装置22aを設け
たものである。石炭の種類により、燃焼灰の組成はほぼ
一定しているので、この灰組成又はCaO/(SiO2
+Al2 O3 )重量比を品質管理装置22aに入力し、
石炭灰のCaO/(SiO2 +Al2 O3 )重量比が
0.06〜0.2の範囲の所定値となるように、かつ、
石膏量が生石灰に換算した石灰の0.2〜1.0倍の範
囲の所定値となるように、供給弁26、30、18を制
御して、混練機32へ供給する石炭灰量、石灰量及び石
膏量を調節する。他の構成及び作用は、実施の第1形態
の場合と同様である。FIG. 3 shows an apparatus for manufacturing civil engineering materials according to a second embodiment of the present invention. This embodiment is the first embodiment.
CaO / (SiO 2 + Al 2 O 3 ) of coal ash burned in a boiler instead of the quality control device 22 in the form
The lime addition amount and the gypsum addition amount to be added to the coal ash are determined from the weight ratio, and a quality control device 22a for controlling the addition amount is provided. Since the composition of the combustion ash is almost constant depending on the type of coal, this ash composition or CaO / (SiO 2
+ Al 2 O 3 ) The weight ratio is input to the quality control device 22a,
The CaO / (SiO 2 + Al 2 O 3 ) weight ratio of the coal ash becomes a predetermined value in the range of 0.06 to 0.2, and
The supply valves 26, 30, and 18 are controlled so that the amount of gypsum becomes a predetermined value in the range of 0.2 to 1.0 times the lime converted to quick lime, and the amount of coal ash supplied to the kneader 32, Adjust the amount and gypsum amount. Other configurations and operations are the same as those in the first embodiment.
【0022】図4は本発明の実施の第3形態による土木
資材製造装置を示している。本実施形態は、排煙脱硫石
膏を粉砕するためのミル40を併設したものである。す
なわち、排煙脱硫石膏は湿潤状態にありハンドリング性
が悪く、かつ、結晶が大きいので、約2倍量の石炭灰を
石炭灰ホッパ24から石炭灰供給機42によりミル40
に供給し、石膏と混合して粉砕する。ミル40として
は、振動ミル、ボールミル、ローラミル等が用いられ
る。なお、石炭灰をミル40に供給する代りに、石灰ホ
ッパ28からの石灰を石灰供給機44を介してミル40
に供給しても良い。石膏と石炭灰との混合粉砕物、又は
石膏と石灰との混合粉砕物は、石膏混合物ホッパ46に
一旦貯留された後、石膏混合物供給機48により固化体
製造プラント20に供給される。品質管理装置22は、
サンプリングされた石炭灰のCaO/(SiO2 +Al
2 O3 )重量比を測定し、測定値に基づいて、CaO/
(SiO2 +Al2 O3)重量比が0.06〜0.2の
範囲の所定値となるように、かつ、石膏量が生石灰に換
算した石灰の0.2〜1.0倍の範囲の所定値となるよ
うに、供給機26、30、42、48、又は供給機2
6、30、44、48を制御して、混練機32へ供給す
る石炭灰量、石灰量及び石膏量を調節する。他の構成及
び作用は、実施の第1形態の場合と同様である。FIG. 4 shows an apparatus for manufacturing civil engineering materials according to a third embodiment of the present invention. In the present embodiment, a mill 40 for crushing flue gas desulfurization gypsum is additionally provided. That is, since the flue gas desulfurization gypsum is in a wet state, the handling property is poor, and the crystal is large, about twice the amount of coal ash is removed from the coal ash hopper 24 by the coal ash feeder 42 into the mill 40.
And mixed with gypsum and crushed. As the mill 40, a vibration mill, a ball mill, a roller mill, or the like is used. Instead of supplying coal ash to the mill 40, lime from the lime hopper 28 is supplied to the mill 40 via the lime feeder 44.
May be supplied. The mixed and pulverized product of gypsum and coal ash or the mixed and pulverized product of gypsum and lime is temporarily stored in the gypsum mixture hopper 46 and then supplied to the solidified body production plant 20 by the gypsum mixture supply device 48. The quality control device 22
CaO / (SiO 2 + Al) of sampled coal ash
2 O 3 ) The weight ratio was measured, and CaO /
(SiO 2 + Al 2 O 3 ) The weight ratio is set to a predetermined value in the range of 0.06 to 0.2, and the amount of gypsum is in the range of 0.2 to 1.0 times the lime converted to quick lime. The feeder 26, 30, 42, 48 or the feeder 2 is set to a predetermined value.
By controlling 6, 30, 44 and 48, the amounts of coal ash, lime and gypsum supplied to the kneader 32 are adjusted. Other configurations and operations are the same as those in the first embodiment.
【0023】図5は本発明の実施の第4形態による土木
資材製造装置を示している。本実施形態は、実施の第3
形態における品質管理装置22の代りに、ボイラで燃焼
させる石炭の灰分のCaO/(SiO2 +Al2 O3 )
重量比から石炭灰に添加する石灰添加量及び石膏添加量
を決定し、添加量を制御する品質管理装置22aを設け
たものである。他の構成及び作用は、実施の第2、3形
態の場合と同様である。FIG. 5 shows a civil engineering material manufacturing apparatus according to a fourth embodiment of the present invention. This embodiment is a third embodiment.
CaO / (SiO 2 + Al 2 O 3 ) of coal ash burned in a boiler instead of the quality control device 22 in the form
The lime addition amount and the gypsum addition amount to be added to the coal ash are determined from the weight ratio, and a quality control device 22a for controlling the addition amount is provided. Other configurations and operations are the same as those of the second and third embodiments.
【0024】図6は本発明の実施の第5形態による土木
資材製造装置を示している。本実施形態は、石灰石又は
/及び貝殻を焼成して生石灰を製造する焼成炉50を併
設したものである。一般に、石炭火力発電所は海に隣接
した地域に設けられており、冷却水としての海水の取出
口等から大量の貝殻が得られるので、この貝殻又は石灰
石を焼成炉50(例えば、流動層炉、シャフト炉等)に
投入し、焼成して生石灰(CaO)を製造し、生石灰ホ
ッパ52に一旦貯留する。この生石灰は粒子状であるの
で、粉砕した後に固化体製造プラント20に供給する必
要がある。このため、生石灰ホッパ52からの生石灰を
生石灰供給機54によりミル56(例えば、振動ミル、
ボールミル、ローラミル等)に供給し、同時に石膏ホッ
パ16からの石膏を石膏供給機18によりミル56に供
給して粉砕し、石膏・生石灰ホッパ58に一旦貯留した
後、石膏・生石灰供給機60により固化体製造プラント
20に供給する。品質管理装置22は、サンプリングさ
れた石炭灰のCaO/(SiO2 +Al2 O3 )重量比
を測定し、測定値に基づいて、CaO/(SiO2 +A
l2 O3)重量比が0.06〜0.2の範囲の所定値と
なるように、かつ、石膏量が生石灰に換算した石灰の
0.2〜1.0倍の範囲の所定値となるように、供給機
26、54、18、60を制御して、混練機32へ供給
する石炭灰量、生石灰量及び石膏量を調節する。本実施
形態では、生石灰の粉砕と石膏の粉砕とをミル56で同
時に行う場合を示しているが、生石灰の粉砕と石膏の粉
砕とを別のミルで、個別に行うように構成する場合もあ
る。この場合は、実施の第3形態におけるように、石膏
は石炭灰の一部と混合されて粉砕されるように構成する
ことが好ましい。他の構成、作用は、実施の第1、3形
態の場合と同様である。FIG. 6 shows an apparatus for manufacturing civil engineering materials according to a fifth embodiment of the present invention. In the present embodiment, a sintering furnace 50 for sintering limestone and / or shells to produce quicklime is additionally provided. Generally, a coal-fired power plant is provided in an area adjacent to the sea, and a large amount of shells can be obtained from an outlet of seawater as cooling water. Therefore, the shells or limestone are converted into a firing furnace 50 (for example, a fluidized bed furnace). , Shaft furnace, etc.), and calcined to produce quicklime (CaO), which is temporarily stored in the quicklime hopper 52. Since this quicklime is in the form of particles, it needs to be supplied to the solidified body manufacturing plant 20 after being pulverized. For this reason, quicklime from the quicklime hopper 52 is milled by the quicklime feeder 54 into a mill 56 (for example, a vibration mill,
The gypsum from the gypsum hopper 16 is simultaneously supplied to the mill 56 by the gypsum feeder 18 to be pulverized, temporarily stored in the gypsum / quick lime hopper 58, and then solidified by the gypsum / quick lime feeder 60. It is supplied to the body manufacturing plant 20. The quality control device 22 calculates the CaO / (SiO 2 + Al 2 O 3 ) weight ratio of the sampled coal ash.
Was measured, based on measurements, CaO / (SiO 2 + A
l 2 O 3 ) The weight ratio is set to a predetermined value in a range of 0.06 to 0.2, and the amount of gypsum is set to a predetermined value in a range of 0.2 to 1.0 times lime converted to quick lime. By controlling the feeders 26, 54, 18, and 60, the amounts of coal ash, quick lime, and gypsum supplied to the kneader 32 are adjusted. In this embodiment, the case where the grinding of the quicklime and the grinding of the gypsum are performed at the same time by the mill 56 is shown. However, the grinding of the quicklime and the grinding of the gypsum may be performed separately by another mill. . In this case, as in the third embodiment, it is preferable that the gypsum is mixed with a part of the coal ash and pulverized. Other configurations and operations are the same as those in the first and third embodiments.
【0025】図7は本発明の実施の第6形態による土木
資材製造装置を示している。本実施形態は、実施の第5
形態における品質管理装置22の代りに、ボイラで燃焼
させる石炭の灰分のCaO/(SiO2 +Al2 O3 )
重量比から石炭に添加する石灰添加量及び石膏添加量を
決定し、添加量を制御する品質管理装置22aを設けた
ものである。他の構成及び作用は、実施の第2、5形態
の場合と同様である。FIG. 7 shows a construction material manufacturing apparatus according to a sixth embodiment of the present invention. This embodiment is the fifth embodiment.
CaO / (SiO 2 + Al 2 O 3 ) of coal ash burned in a boiler instead of the quality control device 22 in the form
A lime addition amount and a gypsum addition amount to be added to coal are determined from a weight ratio, and a quality control device 22a for controlling the addition amount is provided. Other configurations and operations are the same as those in the second and fifth embodiments.
【0026】[0026]
【実施例】以下に、実施例及び比較例を示し、本発明の
特徴とするところをより一層明確にする。 実施例1 表1に示すCaO/(SiO2 +Al2 O3 )重量比が
0.058の石炭灰A100重量部に、消石灰4.6重
量部、ブレーン比表面積が3000cm2 /g の石膏3.
2重量部を加えて、CaO/(SiO2 +Al2 O3 )
重量比を0.10とした混合粉体100重量部に対して
26重量部の温水(50℃)を加えて逆流式高速型混練
機で混練し、混練物を突き固め成形し、ついで、50℃
で15時間養生した後、95℃で15時間養生を行って
固化体を製造した。固化体の圧縮強度は115kg/cm2
であり、有害重金属溶出量も土壌環境基準を満足した。EXAMPLES Examples and comparative examples are shown below to further clarify the features of the present invention. Example 1 Plaster having 4.6 parts by weight of slaked lime and a Blaine specific surface area of 3000 cm 2 / g in 100 parts by weight of coal ash A having a CaO / (SiO 2 + Al 2 O 3 ) weight ratio of 0.058 shown in Table 1.
2 parts by weight, CaO / (SiO 2 + Al 2 O 3 )
26 parts by weight of warm water (50 ° C.) was added to 100 parts by weight of the mixed powder having a weight ratio of 0.10, and the mixture was kneaded with a reverse-flow high-speed kneader, and the kneaded product was compacted and molded. ° C
After curing for 15 hours at 95 ° C., curing was carried out at 95 ° C. for 15 hours to produce a solid. The compressive strength of the solidified body is 115 kg / cm 2
And the amount of harmful heavy metals eluted also met the soil environmental standards.
【0027】[0027]
【表1】 [Table 1]
【0028】実施例2 表1に示すCaO/(SiO2 +Al2 O3 )重量比が
0.025の石炭灰B100重量部に、生石灰4.0重
量部、ブレーン比表面積が3000cm2 /g の石膏3.
0重量部を加えて、CaO/(SiO2 +Al2 O3 )
重量比を0.072とした混合粉体を用いて、実施例1
と同じ条件で固化体を製造した。固化体の圧縮強度は1
00kg/cm2 であり、有害重金属溶出量も土壌環境基準
を満足した。Example 2 As shown in Table 1, 100 parts by weight of coal ash B having a CaO / (SiO 2 + Al 2 O 3 ) weight ratio of 0.025, 4.0 parts by weight of quicklime and a brane specific surface area of 3000 cm 2 / g. Gypsum3.
0 parts by weight, and CaO / (SiO 2 + Al 2 O 3 )
Example 1 was performed using a mixed powder having a weight ratio of 0.072.
A solid was produced under the same conditions as described above. The compressive strength of the solidified body is 1
It was 00 kg / cm 2 , and the harmful heavy metal elution amount also satisfied the soil environmental standard.
【0029】実施例3 石炭灰の気流搬送過程に設けた品質管理装置を用いて、
採取した石炭灰Bの10%スラリーのpHを自動測定した
ところ、10.8であった。この値に基づいて、土木資
材製造装置の消石灰供給量及び石膏供給量をコントロー
ルした。詳しくは、石炭灰85重量部に対し消石灰6重
量部を逆流式高速型混練機に供給し、排煙脱硫石膏3重
量部を石炭灰15重量部とともに振動ミルで粉砕してブ
レーン比表面積を3000cm2 /g とした石膏混合物1
8重量部を上記混練機に供給し、混合粉体のCaO/
(SiO2 +Al2 O3 )重量比を0.079とした。
この混合粉体100重量部に対して24重量部の温水
(50℃)を加えて混練し、混練物を低圧振動成形機で
0.5kg/cm2 Gの圧力で振動を加えながら、□400
×100H 〔mm〕の成形体とし、ついで、約40℃で8
時間、98℃で15時間養生を行い、固化体を製造し
た。固化体の圧縮強度は107kg/cm2 であり、有害重
金属溶出量は土壌環境基準を満足した。Example 3 Using a quality control device provided in the air ash conveying process of coal ash,
When the pH of the 10% slurry of the collected coal ash B was automatically measured, it was 10.8. Based on this value, the slaked lime supply amount and the gypsum supply amount of the civil engineering material production device were controlled. Specifically, 6 parts by weight of slaked lime is supplied to a reverse-flow high-speed kneader with respect to 85 parts by weight of coal ash, and 3 parts by weight of flue gas desulfurization gypsum is pulverized together with 15 parts by weight of coal ash in a vibration mill to have a Blaine specific surface area of 3000 cm. 2 / g and gypsum mixture 1
8 parts by weight were supplied to the kneading machine, and CaO /
The (SiO 2 + Al 2 O 3 ) weight ratio was set to 0.079.
To 100 parts by weight of the mixed powder, 24 parts by weight of warm water (50 ° C.) was added and kneaded, and the kneaded material was shaken at a pressure of 0.5 kg / cm 2 G using a low-pressure vibration molding machine while
× 100H [mm] and then at about 40 ° C
After curing at 98 ° C. for 15 hours, a solid was produced. The solidified body had a compressive strength of 107 kg / cm 2 , and the harmful heavy metal elution amount satisfied the soil environmental standard.
【0030】実施例4 実施例3における固化体をインパクトクラッシャで破砕
し、クラッシャランC−40相当の粒状固化体を得た。
粒状固化体の修正CBRは105%、すり減り減量は3
5%で、砕石路盤材規格を満足した。なお、クラッシャ
ランC−40とは、クラッシャ(破砕機)で割った(破
砕した)後の粒状体で、最大粒径が40mmで路盤材等に
用いられる材料のことを言う。Example 4 The solidified product of Example 3 was crushed by an impact crusher to obtain a granular solidified product equivalent to crusher run C-40.
Modified CBR of granular solidified material is 105%, and abrasion loss is 3
5% satisfied the crushed stone roadbed material standard. The crusher run C-40 is a granular material that has been divided (crushed) by a crusher (crusher) and has a maximum particle size of 40 mm and is a material used for roadbed materials and the like.
【0031】比較例1 本比較例は、石膏添加量が本発明における範囲より少な
い場合の例である。表1に示す石炭灰A100重量部
に、消石灰4.6重量部、石膏0.5重量部を加えて、
実施例1と同じ方法で固化体を製造した。固化体の圧縮
強度は60kg/cm2 であり、有害重金属溶出量はCr6+
が0.06mg/l で、土壌環境基準値の0.05mg/l
を越えた。Comparative Example 1 This comparative example is an example in which the amount of added gypsum is less than the range in the present invention. To 100 parts by weight of coal ash A shown in Table 1, 4.6 parts by weight of slaked lime and 0.5 part by weight of gypsum were added.
A solid was produced in the same manner as in Example 1. The solidified product has a compressive strength of 60 kg / cm 2 and a harmful heavy metal elution amount of Cr 6+.
Is 0.06mg / l, which is 0.05mg / l of the soil environmental standard value.
Crossed.
【0032】比較例2 本比較例は、CaO/(SiO2 +Al2 O3 )重量比
が本発明における範囲より少ない場合の例である。表1
に示す石炭灰B100重量部に、消石灰3.0重量部、
石膏2.0重量部を加えた混合粉体のCaO/(SiO
2 +Al2 O3)重量比を0.052とし、実施例1と
同じ方法で固化体を製造した。固化体の圧縮強度は43
kg/cm2 であり、有害重金属溶出量は、Seが0.01
5mg/lで土壌環境基準値の0.01mg/l を越えた。Comparative Example 2 This comparative example is an example in which the CaO / (SiO 2 + Al 2 O 3 ) weight ratio is smaller than the range in the present invention. Table 1
, 3.0 parts by weight of slaked lime,
CaO / (SiO of mixed powder to which gypsum 2.0 parts by weight was added
2 + Al 2 O 3 ) A solidified body was produced in the same manner as in Example 1 except that the weight ratio was 0.052. The compressive strength of the solidified material is 43
kg / cm 2 , and the amount of harmful heavy metals eluted is 0.01 for Se.
5 mg / l exceeded the soil environmental standard of 0.01 mg / l.
【0033】[0033]
【発明の効果】本発明は上記のように構成されているの
で、つぎのような効果を奏する。 (1) 石炭灰を主原料とする固化体の製造時の石灰添
加量及び石膏添加量を、石炭灰のCaO/(SiO2 +
Al2 O3 )重量比が一定値になるように、かつ、石膏
量が生石灰の一定倍になるように制御して適正量とする
ことにより、効率よく目標強度の固化体を得ることがで
きる。 (2) 固化体製造時の石灰添加量及び石膏添加量を適
正量(最小量)とすることで、固化体製造コストを最小
限に抑えることができる。また、相対的に大量の石炭灰
を処理することができる。 (3) 多炭種灰に対応することができ、石炭灰性状に
よらず所定品質の固化体が安定的に得られ、路盤材、埋
立資材等の土木資材として有効利用することができる。 (4) 固化体製造時に必要な石灰、燃料等を石炭焚火
力発電所からの廃棄物でまかなうように構成する場合
は、発電所のゼロエミッションを図ることができる。As described above, the present invention has the following effects. (1) The amount of lime added and the amount of gypsum added during the production of a solidified product using coal ash as a main raw material are determined by the CaO / (SiO 2 +
(Al 2 O 3 ) By controlling the weight ratio to be a constant value and controlling the amount of gypsum to be a constant multiple of quicklime to an appropriate amount, it is possible to efficiently obtain a solidified body having a target strength. . (2) By setting the added amount of lime and the added amount of gypsum at the time of producing the solidified product to an appropriate amount (minimum amount), the cost of producing the solidified product can be minimized. Also, a relatively large amount of coal ash can be treated. (3) It is possible to cope with multi-charcoal seed ash, a solid of predetermined quality is stably obtained irrespective of the properties of coal ash, and it can be effectively used as a civil engineering material such as a roadbed material and a landfill material. (4) If the lime, fuel, etc., required for the production of solidified material are covered by the waste from the coal-fired power plant, the power plant can achieve zero emissions.
【図面の簡単な説明】[Brief description of the drawings]
【図1】本発明の実施の第1形態による石炭灰を主原料
とする土木資材の製造装置を示す概略構成図である。FIG. 1 is a schematic configuration diagram showing an apparatus for producing civil engineering materials using coal ash as a main raw material according to a first embodiment of the present invention.
【図2】図1における固化体製造プラントの一例を示す
概略構成図である。FIG. 2 is a schematic configuration diagram showing an example of a solidified body production plant in FIG.
【図3】本発明の実施の第2形態による石炭灰を主原料
とする土木資材の製造装置を示す概略構成図である。FIG. 3 is a schematic configuration diagram showing an apparatus for manufacturing civil engineering materials using coal ash as a main raw material according to a second embodiment of the present invention.
【図4】本発明の実施の第3形態による石炭灰を主原料
とする土木資材の製造装置を示す概略構成図である。FIG. 4 is a schematic configuration diagram showing an apparatus for producing civil engineering materials using coal ash as a main raw material according to a third embodiment of the present invention.
【図5】本発明の実施の第4形態による石炭灰を主原料
とする土木資材の製造装置を示す概略構成図である。FIG. 5 is a schematic configuration diagram showing an apparatus for producing civil engineering materials using coal ash as a main raw material according to a fourth embodiment of the present invention.
【図6】本発明の実施の第5形態による石炭灰を主原料
とする土木資材の製造装置を示す概略構成図である。FIG. 6 is a schematic configuration diagram showing an apparatus for producing civil engineering materials using coal ash as a main raw material according to a fifth embodiment of the present invention.
【図7】本発明の実施の第6形態による石炭灰を主原料
とする土木資材の製造装置を示す概略構成図である。FIG. 7 is a schematic configuration diagram showing an apparatus for producing civil engineering materials using coal ash as a main raw material according to a sixth embodiment of the present invention.
10 ボイラ 12 電気集塵機 14 脱硫装置 16 石膏ホッパ 18 石膏供給機 20 固化体製造プラント 22、22a 品質管理装置 24 石炭灰ホッパ 26、42 石炭灰供給機 28 石灰ホッパ 30、44 石灰供給機 32 混練機 34 成形機 36 養生装置 38 破砕機 40、56 ミル 46 石膏混合物ホッパ 48 石膏混合物供給機 50 焼成炉 52 生石灰ホッパ 54 生石灰供給機 58 石膏・生石灰ホッパ 60 石膏・生石灰供給機 DESCRIPTION OF SYMBOLS 10 Boiler 12 Electric dust collector 14 Desulfurization apparatus 16 Gypsum hopper 18 Gypsum supply machine 20 Solidified body manufacturing plant 22, 22a Quality control apparatus 24 Coal ash hopper 26, 42 Coal ash supply machine 28 lime hopper 30, 44 Lime supply machine 32 Kneader 34 Molding machine 36 curing device 38 crusher 40, 56 mill 46 gypsum mixture hopper 48 gypsum mixture feeder 50 firing furnace 52 quick lime hopper 54 quick lime feeder 58 gypsum / quick lime hopper 60 gypsum / quick lime feeder
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C04B 22:14) (56)参考文献 特開 昭56−155064(JP,A) 特開 昭48−93620(JP,A) 特開 昭57−92560(JP,A) 特開 平9−156971(JP,A) 特開 平9−262276(JP,A) (58)調査した分野(Int.Cl.7,DB名) C04B 7/00 - 28/36 B09B 3/00 ────────────────────────────────────────────────── (5) Continuation of the front page (51) Int.Cl. 7 Identification code FI C04B 22:14) (56) References JP-A-56-1555064 (JP, A) JP-A-48-93620 (JP, A) JP-A-57-92560 (JP, A) JP-A-9-156971 (JP, A) JP-A-9-262276 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C04B 7/00-28/36 B09B 3/00
Claims (10)
3 )重量比が水和反応が十分に進行し、かつSiO 2 及
びAl 2 O 3 不足とならない範囲である0.06〜0.
2となるように石灰を加えて調整混合物とするととも
に、この調整混合物に水和反応が十分に進行し、かつ未
反応の石膏が残存しない範囲である生石灰に換算した石
灰の0.2〜1.0倍の重量の石膏を加えて石膏調整混
合物とし、同時にこの石膏調整混合物に混練水を加えて
混練した後、混練物を成形し、ついで、成形物を常温〜
55℃で養生した後、水蒸気養生して、最低限の添加材
量で高強度の固化体を得ることを特徴とする石炭灰を主
原料とする土木資材の製造方法。1. Coal ash contains CaO / (SiO 2 + Al 2 O)
3) the weight ratio of the hydration reaction proceeds sufficiently, and SiO 2 及
A range that does not fine Al 2 O 3 and lack 0.06 to 0.
Lime is added to obtain an adjusted mixture, and the adjusted mixture is sufficiently hydrated, and
A gypsum of 0.2 to 1.0 times the weight of lime converted to quick lime, which is a range in which the gypsum of the reaction does not remain, is added to a gypsum adjustment mixture, and at the same time, kneading is performed by adding kneading water to the gypsum adjustment mixture. The kneaded product is molded, and then the molded product is brought to room temperature to
After curing at 55 ° C, steam curing to minimize the amount of additive
A method for producing a civil engineering material using coal ash as a main raw material, characterized in that a high-strength solidified body is obtained in an amount .
状固化体とする請求項1記載の石炭灰を主原料とする土
木資材の製造方法。2. The method according to claim 1, wherein the solidified material is crushed into a granular solidified material having a particle size of 40 mm or less.
いる請求項1又は2記載の石炭灰を主原料とする土木資
材の製造方法。3. The method according to claim 1, wherein warm water of 30 to 60 ° C. is used as the kneading water.
ボイラで燃焼させる石炭の灰分のCaO/(SiO2 +
Al2 O3 )重量比に基づいて制御する請求項1、2又
は3記載の石炭灰を主原料とする土木資材の製造方法。4. The amount of lime and gypsum added to coal ash,
CaO / (SiO 2 +
4. The method according to claim 1, wherein the control is based on the weight ratio of Al 2 O 3 ).
取し、石炭灰のCaO/(SiO2 +Al2 O3 )重量
比の測定を行い、該測定値に基づいて石灰及び石膏の添
加量を制御する請求項1〜4のいずれかに記載の石炭灰
を主原料とする土木資材の製造方法。5. collected coal ash hopper or under pneumatic conveying process performs measurement of CaO / (SiO 2 + Al 2 O 3) ratio by weight of the coal ash, the addition of lime and gypsum based on the measured value A method for producing a civil engineering material using coal ash as a main raw material according to claim 1, wherein the amount is controlled.
石膏を用い、この石膏を石炭灰の一部又は石灰の一部と
ともに粉砕して、ブレーン比表面積を2500cm2 /g
以上としたものを石炭灰に添加する請求項1〜5のいず
れかに記載の石炭灰を主原料とする土木資材の製造方
法。6. A gypsum obtained from a flue gas desulfurization unit is used as the gypsum, and this gypsum is pulverized together with a part of coal ash or a part of lime to have a Blaine specific surface area of 2500 cm 2 / g.
The method for producing a civil engineering material using coal ash as a main raw material according to any one of claims 1 to 5, wherein the above-mentioned components are added to coal ash.
もいずれかを焼成して生石灰とし、この生石灰を粉砕し
てブレーン比表面積を2500cm2 /g 以上としたもの
を用いる請求項1〜6のいずれかに記載の石炭灰を主原
料とする土木資材の製造方法。7. The lime according to claim 1, wherein at least one of limestone and shells is calcined to form quicklime, and the quicklime is pulverized to a Blaine specific surface area of 2500 cm 2 / g or more. A method for producing civil engineering materials using coal ash as a main raw material.
ガス中に含まれる石炭灰を捕集する集塵機と、捕集され
た石炭灰を導入し石灰、石膏及び水とともに混練する混
練機と、混練機からの混練物を成形する成形機と、成形
機からの成形物を養生する養生装置とを備えた石炭灰処
理装置において、 ホッパ又は気流搬送過程で採取された石炭灰のCaO/
(SiO2 +Al2 O3 )重量比の測定を行う品質管理
装置を設け、この品質管理装置により石炭灰に添加する
石灰及び石膏の量を制御することができるように、この
品質管理装置と石灰供給機及び石膏供給機とが連動接続
されて、石炭灰−石灰−石膏系混合物からなる固化体を
得るようにしたことを特徴とする石炭灰を主原料とする
土木資材の製造装置。8. A dust collector for introducing flue gas from a coal-fired boiler and collecting coal ash contained in the flue gas, a kneader for introducing the collected coal ash and kneading it with lime, gypsum and water; In a coal ash processing apparatus provided with a molding machine for molding a kneaded product from a kneading machine and a curing device for curing the molded product from the molding machine, the CaO / CaO /
The quality control device for performing measurements of (SiO 2 + Al 2 O 3 ) ratio by weight is provided to be able to control the amount of lime and gypsum to be added to the coal ash by the quality control apparatus, and the quality control device An apparatus for manufacturing civil engineering materials using coal ash as a main raw material, wherein a lime feeder and a gypsum feeder are interlocked and connected to obtain a solidified body composed of a coal ash-lime-gypsum-based mixture.
ガス中に含まれる石炭灰を捕集する集塵機と、捕集され
た石炭灰を導入し石灰、石膏及び水とともに混練する混
練機と、混練機からの混練物を成形する成形機と、成形
機からの成形物を養生する養生装置とを備えた石炭灰処
理装置において、 前記石炭焚ボイラで燃焼させる石炭の炭種の灰分組成か
らCaO/(SiO2+Al2 O3 )重量比を計算し石
炭灰に添加する石灰及び石膏の量を決定する品質管理装
置を設け、この品質管理装置により石炭灰に添加する石
灰及び石膏の量を制御することができるように、この品
質管理装置と石灰供給機及び石膏供給機とが連動接続さ
れて、石炭灰−石灰−石膏系混合物からなる固化体を得
るようにしたことを特徴とする石炭灰を主原料とする土
木資材の製造装置。9. A dust collector for introducing exhaust gas from a coal-fired boiler and collecting coal ash contained in the exhaust gas, a kneader for introducing the collected coal ash and kneading it with lime, gypsum and water; In a coal ash processing apparatus including a molding machine for molding a kneaded product from a kneading machine and a curing device for curing a molded product from the molding machine, a CaO composition based on the ash composition of a coal type of coal to be burned in the coal-fired boiler. / (SiO 2 + Al 2 O 3 ) Calculate weight ratio to determine the amount of lime and gypsum added to coal ash, and control the amount of lime and gypsum added to coal ash by this quality control device The lime feeder and the gypsum feeder are linked and connected to each other so as to obtain a solidified material composed of a coal ash-lime-gypsum-based mixture. Made from soil Materials for manufacturing equipment.
ための破砕機を設けて、石炭灰−石灰−石膏混合物から
なる粒状の固化体を得るようにした請求項8又は9記載
の石炭灰を主原料とする土木資材の製造装置。10. The method according to claim 8, wherein a crusher for crushing the living organisms is provided downstream of the curing device so as to obtain a granular solidified substance composed of a coal ash-lime-gypsum mixture. Manufacturing equipment for civil engineering materials using coal ash as a main raw material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30644897A JP3200811B2 (en) | 1997-10-20 | 1997-10-20 | Manufacturing method and apparatus for civil engineering materials using coal ash as a main raw material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30644897A JP3200811B2 (en) | 1997-10-20 | 1997-10-20 | Manufacturing method and apparatus for civil engineering materials using coal ash as a main raw material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH11116292A JPH11116292A (en) | 1999-04-27 |
| JP3200811B2 true JP3200811B2 (en) | 2001-08-20 |
Family
ID=17957131
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP30644897A Expired - Fee Related JP3200811B2 (en) | 1997-10-20 | 1997-10-20 | Manufacturing method and apparatus for civil engineering materials using coal ash as a main raw material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3200811B2 (en) |
Families Citing this family (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6520099B1 (en) | 1999-11-04 | 2003-02-18 | Idemitsu Kosan Co., Ltd. | Method for treating combustion ash of coal and method for desulfurization |
| JP4524721B2 (en) * | 2000-04-10 | 2010-08-18 | 株式会社前田先端技術研究所 | Cement composition containing rice husk ash etc. |
| JP3773793B2 (en) * | 2001-01-09 | 2006-05-10 | 財団法人石炭利用総合センター | Method and apparatus for controlling quality of solidified body using coal ash as raw material |
| JP4725302B2 (en) * | 2005-11-21 | 2011-07-13 | Jfeスチール株式会社 | Method for treating eluted component-containing substance, stabilizing material and method for producing the same |
| JP5081426B2 (en) * | 2006-10-25 | 2012-11-28 | 川崎重工業株式会社 | Method and apparatus for producing granular solid using coal ash as raw material |
| JP5765527B2 (en) * | 2011-03-24 | 2015-08-19 | 東京電力株式会社 | Method for producing solidified body for water retention roadbed material |
| JP5888765B2 (en) * | 2011-03-30 | 2016-03-22 | 一般財団法人電力中央研究所 | Coal ash compaction granulator |
| CN103419271A (en) * | 2012-05-23 | 2013-12-04 | 北京航空航天大学 | Preparation method of calcium silicate board |
| JP6230040B2 (en) * | 2013-03-29 | 2017-11-15 | 一般財団法人電力中央研究所 | Kneaded product production equipment |
| JP2016222494A (en) * | 2015-05-29 | 2016-12-28 | 一般財団法人電力中央研究所 | Method for producing solidified coal ash |
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| JP6733345B2 (en) * | 2016-06-20 | 2020-07-29 | 宇部興産株式会社 | Coal ash treatment method |
| CN106734064B (en) * | 2016-11-29 | 2023-08-04 | 贵阳开磷化肥有限公司 | Phosphogypsum harmless treatment device and phosphogypsum harmless treatment method for wet-process phosphoric acid output |
| CN111605062B (en) * | 2019-09-10 | 2021-08-13 | 北新集团建材股份有限公司 | A gypsum-based decorative material molding system and molding method |
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-
1997
- 1997-10-20 JP JP30644897A patent/JP3200811B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH11116292A (en) | 1999-04-27 |
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